US4127503A - Oxygen absorbent - Google Patents
Oxygen absorbent Download PDFInfo
- Publication number
- US4127503A US4127503A US05/816,134 US81613477A US4127503A US 4127503 A US4127503 A US 4127503A US 81613477 A US81613477 A US 81613477A US 4127503 A US4127503 A US 4127503A
- Authority
- US
- United States
- Prior art keywords
- weight
- powder
- parts
- metal
- absorbent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B55/00—Preserving, protecting or purifying packages or package contents in association with packaging
- B65B55/02—Sterilising, e.g. of complete packages
- B65B55/12—Sterilising contents prior to, or during, packaging
- B65B55/19—Sterilising contents prior to, or during, packaging by adding materials intended to remove free oxygen or to develop inhibitor gases, e.g. vapour phase inhibitors
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
- A23L3/34—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by treatment with chemicals
- A23L3/3409—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by treatment with chemicals in the form of gases, e.g. fumigation; Compositions or apparatus therefor
- A23L3/3418—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by treatment with chemicals in the form of gases, e.g. fumigation; Compositions or apparatus therefor in a controlled atmosphere, e.g. partial vacuum, comprising only CO2, N2, O2 or H2O
- A23L3/3427—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by treatment with chemicals in the form of gases, e.g. fumigation; Compositions or apparatus therefor in a controlled atmosphere, e.g. partial vacuum, comprising only CO2, N2, O2 or H2O in which an absorbent is placed or used
- A23L3/3436—Oxygen absorbent
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
Definitions
- This invention relates to an oxygen absorbent comprising a metal powder coated with a definite amount of a metal halide and having a minor amount of water.
- Molds or eumycetes, bacterias and higher organisms such as insects tend to disturb preservation of foodstuffs. These mold eumycetes, bacterias and insects live and grow in the presence of oxygen and cause putrefaction and change in quality of foodstuffs.
- Japanese patent publication No. 19729/1972 discloses the use of an oxygen absorbent comprising hydrosulfite, calcium hydroxide, sodium bicarbonate, activated carbon and optionally water to preserve vegetables by removing oxygen from atmosphere.
- U.S. Pat. No. 2,825,651 proposes a process for preparing an oxygen absorbent comprising mixing a finely divided sulfite and a finely divided metal salt, at least one of the two compounds having water of crystallization and compression-pelletizing the mixture in order to increase the rate of the oxidation of sulfite.
- British Pat. No. 553,991 discloses the step of forming pilule comprising carbon and highly activated iron powder obtained by hydrogen treatment followed by absorbing oxygen in a hood using the resulting pilule. Since iron powder contained in the pilule is highly active, the iron intensely reacts with oxygen in the container to remove oxygen therein. There is the possibility of fire in case of using such highly active iron powder. The process of British Pat. No. 5553991 is dangerous.
- Foodstuffs contain a considerable amount of water, and when a foodstuff is placed in a sealed container, it was found that moisture fills the container to nearly saturated humidity at the temperature. It was also found that when a dry mixture of a metal powder and a metal halide is sealed with water-containing foodstuffs in a container, the oxygen concentration in the container gradually lowers until at last the concentration is zero.
- the present inventors also found that when a mixture of a metal powder and a metal halide is used, a large amount of the metal halide is required for rapidly absorbing oxygen but that when the metal halide is coated on the metal powder, a small amount of the metal halide is effective for rapidly absorbing oxygen.
- an oxygen absorbent powder in which a small amount of the metal halide is coated on the surface of metal powder and which has a minor water content rapidly absorbs oxygen in a sealed container, when it coexists with foodstuffs.
- the oxygen absorbent has free flowability and minor water content, it has the following advantages:
- an oxygen absorbent obtained by coating a metal halide and a binder and/or an alkaline material on the surface of a metal powder has an excellent ability to absorb oxygen and generates little hydrogen.
- This invention is formed on the basis of this discovery.
- an object of this invention is to provide an oxygen absorbent overcoming the prior art disadvantages, namely non-flowability, dangerousness and wettability.
- This invention relates to an oxygen absorbent in which at least one metal halide is coated on the surface of at least one metal powder, the amount of metal halide coated being in the range of from about 0.001 part to about 10 parts by weight on the basis of 100 parts by weight of the metal powder, and the water content of the absorbent being less than 1% by weight on the basis of the total weight of the absorbent; and this invention also relates to an oxygen absorbent in which at least one metal halide and at least one binder and/or at least one alkaline material is coated on the surface of at least one metal powder, the amount of metal halide coated being in the range of from about 0.001 part to about 10 parts by weight on the basis of 100 parts by weight of the metal powder, and the water content of the absorbent being less than 1% by weight on the basis of the total weight of the absorbent.
- This invention further relates to a process for producing an oxygen absorbent which comprises mixing at least one metal powder with a solution of at least one metal halide to coat 0.001 part to 10 parts by weight of the metal halide on 100 parts by weight of the metal powder, and drying the coating material until the water content thereof amounts to less than 1% by weight of the total weight of the absorbent; and this invention relates to a process for producing an oxygen absorbent which comprises mixing at least one metal powder with at least one metal halide solution and at least one binder and/or at least one alkaline material to coat 0.001 part to 10 parts by weight of the metal halide and the binder and/or the alkaline material on 100 parts of the metal powder, and drying the coating material until the water content thereof amounts to less than 1% by weight based on the total weight of the absorbent.
- oxygen absorbent in the specification and the claim means an agent for removing oxygen.
- the metal powders which can be employed in the present invention may include copper powder, iron powder, zinc powder, and mixtures thereof; iron powder is preferred.
- the metal powder has size of less than 10 mesh, preferably 50 mesh.
- the metal powders may be electrolyic metal powders reduced metal powders atomized metal powders and stamped metal powders. Reduced iron powder, electrolytic iron powder and spraying iron powder are preferred.
- the metal does not need to have high purity.
- the metal may contain impurities, as long as the object of this invention can be achieved.
- the mesh screen employed was Tyler Standard Sieve.
- the metals constituting the metal halides may be metals selected from the group consisting of alkali metals, alkali earth metals, copper, zinc, aluminum, tin, manganese, iron, cobalt and nickel.
- alkali metals such as lithium, sodium, potassium and alkali earth metals, such as calcium, magnesium and barium are preferred.
- the halogen constituting the metal halide may be chlorine, bromine or iodine. Chlorine is preferred.
- the amount of the metal halide to be coated on the surface of the metal powder is in the range of from about 0.001 part to about 10 parts by weight per 100 parts by weight of metal powder, and about 0.01 part to about 5 parts of the metal halide is preferred.
- the amount of the metal halide coated is less than 0.001 part by weight, the absorbing ability of oxygen is lowered.
- the amount of the metal halide coated is more than 10 parts by weight, much water is likely to be migrated into the oxygen absorbent due to deliquescence of the metal halide. Therefore, the metal halide penetrates through the packaging material into foodstuff and the evolution of hydrogen increases.
- the binders may include water soluble polymeric compounds, such as sodium alginate, carboxymethyl cellulose (CMC), hydroxymethyl cellulose, methyl cellulose, ethyl cellulose, propyl cellulose, sodium carboxymethyl cellulose, starch, polyhydric alcohols, polyvinyl alcohol (PVA), saccharides, tragacanth gum.
- the amount of the binder employed may be in the range of from about 0.01 part to 10 parts by weight per 100 parts by weight of the metal powder, and about 0.1 to about 2 parts by weight of the binder is preferably employed.
- the alkaline materials may include hydroxides, carbonates, sulfites, thiosulfates, dibasic phosphates, tribasic phosphates, polyphosphates, tri-polyphosphates, or organic acid salts of alkali metals or alkali earth metals.
- the amount of the alkaline material employed may be in the range of about 0.01 part to about 10 parts by weight, preferably about 0.1 part to about 2 parts per 100 parts of the metal powder.
- water content in the specification and the claims means content of free water, and excludes content of water of crystallization.
- the oxygen absorbent of this invention has less than 1% of free water on the basis of the total weight of the absorbent, preferably less than 0.5% by weight of water, and more preferably less than 0.2% by weight of water.
- the oxygen absorbent of this invention is prepared in the following way:
- the metal powder is mixed with a solution of the metal halide and optionally the binder and/or the alkaline material, thereby coating the metal halide and optionally the binder and/or the alkaline material on the surface of the metal powder; and the resulting coating is dried until the water content thereof amounts to less than 1% by weight based on the total weight of the absorbent.
- the solution of the metal halide may be a conventional aqueous solution thereof.
- the metal halide may be dissolved in mixture of water and other solvent.
- the halide concentration may be suitably selected from any concentration up to saturated concentration.
- the metal powder is mixed with the solution of the metal halide until the halide is coated on the powder particle.
- the order of the coating is not critical.
- the metal powder may be coated with these materials simultaneously or successively.
- the mixing process and the coating process are not critical.
- the mixture of the metal powder and the solution of the metal halide and other component may be dried as it is, or after the mixture is filtered, the precipitate may be dried.
- the metal powder is mixed with the solution of the metal halide and optionally the binder and/or the alkaline material containing a minor amount of water; and the resulting mixture is dried as it is.
- the coating is dried until the water content amounts to less than 1%, preferably less than 0.5%, more preferably less than 0.2% and most preferably is substantially zero.
- the water content is more than 1%, the resulting absorbent has poor flowability, it is difficult to pack the absorbent, it penetrates through the packaging material and the amount of hydrogen evoluted becomes more.
- the coating may be dried under an inert gas atmosphere, one atmospheric pressure or a reduced pressure.
- the metal halide, and optionally the binder and/or the alkaline material are dissolved in the mixture of water and a hydrophilic solvent, such as an alcohol.
- the oxygen obsorbent of this invention can be employed under moisture-rich atmosphere, preferably under an atmosphere having a relative humidity of more than 50%. Therefore, it can be profitably employed in a sealed container in which water-containing foodstuffs are packed. In case of packing foodstuffs containing little or no water, the absorbent can be profitably employed with water-containing materials or compounds having water of hydration or crystallization. Also, it can be employed with materials generating water in the packaging system.
- the oxygen absorbent of this invention is powder, and the powder absorbent may be employed as it is. Since the moldability of the absorbent is good, the absorbent powder can be tableted by tableting machine. The resulting tablet has good hardness and has the absorbing ability of oxygen as the absorbent powder does.
- the oxygen absorbent of this invention is prepared by coating the metal halide on the surface of the metal powder, the metal powder and the metal halide contact each other very effectively. Therefore, although the amount of the halide employed is small, the absorbing ability of oxygen is large. Since the amount of the halide employed is small, the absorbent of this invention becomes neither wet nor pasty and, it does not remove a large amount of water from the foodstuff, whereby the degradation of the foodstuff is prevented, and the absorbent neither penetrates into the packaging material nor contaminates the foodstuffs.
- the oxygen absorbent of this invention Since the oxygen absorbent of this invention has a low water content, it does not absorb oxygen at all even when it is allowed to stand in air. Handling of the absorbent is easy, and little hydrogen is generated in storage or during use of the absorbent.
- oxygen absorbent of this invention Only when the oxygen absorbent of this invention is sealed with water-containing foodstuff in a container, it exhibits the absorbing ability of oxygen. Oxygen absorbents having a variety of absorbing properties can be obtained by varying its components and its proportion.
- the oxygen absorbent of this invention is practical and has excellent properties.
- the compound absorbed little oxygen.
- the amount of oxygen absorbed of the compound employed in Comparative Example 2 was less than that of the absorbent of Example 1.
- the concentration of hydrogen evoluted in the sealed container was 0.32% after 80 hours passed.
- the concentration of hydrogen evoluted in the sealed container was 2.3% after 80 hours passed. The value was more than that in Example 1.
- the concentration of hydrogen evolved in the sealed container was 3.1%. The amount was much. Stain on the paper not due to the penetration of the compound into the paper was detected two days after the compound was set to absorb oxygen. Black stain on the all portion of paper in contact with the powder was detected in four days.
- test bread gets moldy was evaluated by the following four degree scale.
- Sponge cake (Preservating temperature was 25° C.).
- the resulting metal halide-coated metal powder was placed in a perforated polyethylene film-laminated paper bag.
- the bag and sanitary cotton impregnated with 10 ml. of water were placed in a 1l. sealed container so as not to contact the bag with the cotton.
- the container was left to stand at 25° C. After 30 hours passed, the oxygen concentration was 0.0%. After 80 hours passed, the hydrogen concentration was 0.0003%.
- Example 11 One gram of the powder obtained in Example 11 was placed in a perforated polyethylene film-laminated paper bag. The bag was left to stand for 6 months in a room maintained at a relative humidity of 50-60%. Thereafter, the bag and sanitary cotton impregnated with 10 ml. of water were placed in a 1l. sealed container so as not to contact the bag with the cotton. The amount of oxygen absorbed was measured at 25° C. periodically. The results are shown in Table 19.
- the concentration of hydrogen generated after 80 hours was 0.006%.
- Example 1 The amount of oxygen absorbed was lowered in comparison with Example 1.
- the resulting powder consisted of the NaCl-coated Fe powder and white NaCl crystal, and had poor flowability. Since the powder is deliquescent, it was impossible to fill paper bags with the powder automatically by automatic filling machine.
Abstract
An oxygen absorbent comprising a metal powder and a metal halide coated thereon is disclosed.
Description
This invention relates to an oxygen absorbent comprising a metal powder coated with a definite amount of a metal halide and having a minor amount of water.
In order to preserve foodstuffs, such as vegetables, fish, shellfish, meats, processed foodstuffs, such as potato chips, cakes, peanuts, etc., and so on, it is necessary to prevent the foodstuff's from getting moldy and from putrefying. Prior art methods have used freezer storage, cold storage, vacuum packaging and replacing the gas present in the inner part of packaging by an inert gas for preventing foodstuffs from getting moldy and putrefying. Additives, such as antioxidant, have been used for preserving foodstuffs. Recently, governments have started to regulate the use of additives for food, since it is realized that some additives are injurious to humans. The freezer storage method requires large-scale apparatus and complicated operation, so the freezer storage method is costly.
Molds or eumycetes, bacterias and higher organisms such as insects tend to disturb preservation of foodstuffs. These mold eumycetes, bacterias and insects live and grow in the presence of oxygen and cause putrefaction and change in quality of foodstuffs.
Therefore, if oxygen can be selectively removed from the atmosphere in which the foodstuffs are packed, the problem of putrefaction and change in quality of foodstuff can be overcome, and it will become possible to preserve foodstuffs for a long time.
Attempts have been made for producing such an oxygen absorbent.
Japanese patent publication No. 19729/1972 discloses the use of an oxygen absorbent comprising hydrosulfite, calcium hydroxide, sodium bicarbonate, activated carbon and optionally water to preserve vegetables by removing oxygen from atmosphere.
U.S. Pat. No. 2,825,651 proposes a process for preparing an oxygen absorbent comprising mixing a finely divided sulfite and a finely divided metal salt, at least one of the two compounds having water of crystallization and compression-pelletizing the mixture in order to increase the rate of the oxidation of sulfite.
British Pat. No. 553,991 discloses the step of forming pilule comprising carbon and highly activated iron powder obtained by hydrogen treatment followed by absorbing oxygen in a hood using the resulting pilule. Since iron powder contained in the pilule is highly active, the iron intensely reacts with oxygen in the container to remove oxygen therein. There is the possibility of fire in case of using such highly active iron powder. The process of British Pat. No. 5553991 is dangerous.
The present inventors have carried out wide researches on an oxygen absorbent having the following properties:
(a) having no risk from hydrogen-evolution,
(b) being capable of being packed by automatic packaging machine,
(c) being free-flowing,
(d) and, maintaining the effectiveness of the effective component contained therein, even when the absorbent is allowed to stand in air before being sealed with foodstuffs.
Foodstuffs contain a considerable amount of water, and when a foodstuff is placed in a sealed container, it was found that moisture fills the container to nearly saturated humidity at the temperature. It was also found that when a dry mixture of a metal powder and a metal halide is sealed with water-containing foodstuffs in a container, the oxygen concentration in the container gradually lowers until at last the concentration is zero.
The present inventors also found that when a mixture of a metal powder and a metal halide is used, a large amount of the metal halide is required for rapidly absorbing oxygen but that when the metal halide is coated on the metal powder, a small amount of the metal halide is effective for rapidly absorbing oxygen. In other words, it was found that an oxygen absorbent powder in which a small amount of the metal halide is coated on the surface of metal powder and which has a minor water content rapidly absorbs oxygen in a sealed container, when it coexists with foodstuffs.
It was found that since the oxygen absorbent has free flowability and minor water content, it has the following advantages:
(a) Since it absorbs oxygen while taking a small amount of water from the foodstuffs, little of the water contained in the oxygen absorbent migrates into the foodstuffs contrary to the prior art oxygen absorbent,
(b) It does not become wet and pasty, and
(c) It does not penetrates through the packaging material into the foodstuff.
It was also found that little hydrogen is evoluted.
The present inventors further found that an oxygen absorbent obtained by coating a metal halide and a binder and/or an alkaline material on the surface of a metal powder has an excellent ability to absorb oxygen and generates little hydrogen.
This invention is formed on the basis of this discovery.
Therefore, an object of this invention is to provide an oxygen absorbent overcoming the prior art disadvantages, namely non-flowability, dangerousness and wettability.
This invention relates to an oxygen absorbent in which at least one metal halide is coated on the surface of at least one metal powder, the amount of metal halide coated being in the range of from about 0.001 part to about 10 parts by weight on the basis of 100 parts by weight of the metal powder, and the water content of the absorbent being less than 1% by weight on the basis of the total weight of the absorbent; and this invention also relates to an oxygen absorbent in which at least one metal halide and at least one binder and/or at least one alkaline material is coated on the surface of at least one metal powder, the amount of metal halide coated being in the range of from about 0.001 part to about 10 parts by weight on the basis of 100 parts by weight of the metal powder, and the water content of the absorbent being less than 1% by weight on the basis of the total weight of the absorbent.
This invention further relates to a process for producing an oxygen absorbent which comprises mixing at least one metal powder with a solution of at least one metal halide to coat 0.001 part to 10 parts by weight of the metal halide on 100 parts by weight of the metal powder, and drying the coating material until the water content thereof amounts to less than 1% by weight of the total weight of the absorbent; and this invention relates to a process for producing an oxygen absorbent which comprises mixing at least one metal powder with at least one metal halide solution and at least one binder and/or at least one alkaline material to coat 0.001 part to 10 parts by weight of the metal halide and the binder and/or the alkaline material on 100 parts of the metal powder, and drying the coating material until the water content thereof amounts to less than 1% by weight based on the total weight of the absorbent.
The term "oxygen absorbent" in the specification and the claim means an agent for removing oxygen.
The metal powders which can be employed in the present invention may include copper powder, iron powder, zinc powder, and mixtures thereof; iron powder is preferred. Suitably the metal powder has size of less than 10 mesh, preferably 50 mesh. The metal powders may be electrolyic metal powders reduced metal powders atomized metal powders and stamped metal powders. Reduced iron powder, electrolytic iron powder and spraying iron powder are preferred. The metal does not need to have high purity. The metal may contain impurities, as long as the object of this invention can be achieved. The mesh screen employed was Tyler Standard Sieve.
The metals constituting the metal halides may be metals selected from the group consisting of alkali metals, alkali earth metals, copper, zinc, aluminum, tin, manganese, iron, cobalt and nickel. In order to avoid the generation of hydrogen, alkali metals, such as lithium, sodium, potassium and alkali earth metals, such as calcium, magnesium and barium are preferred. The halogen constituting the metal halide may be chlorine, bromine or iodine. Chlorine is preferred.
The amount of the metal halide to be coated on the surface of the metal powder is in the range of from about 0.001 part to about 10 parts by weight per 100 parts by weight of metal powder, and about 0.01 part to about 5 parts of the metal halide is preferred. When the amount of the metal halide coated is less than 0.001 part by weight, the absorbing ability of oxygen is lowered. When the amount of the metal halide coated is more than 10 parts by weight, much water is likely to be migrated into the oxygen absorbent due to deliquescence of the metal halide. Therefore, the metal halide penetrates through the packaging material into foodstuff and the evolution of hydrogen increases.
Suitably, the binders may include water soluble polymeric compounds, such as sodium alginate, carboxymethyl cellulose (CMC), hydroxymethyl cellulose, methyl cellulose, ethyl cellulose, propyl cellulose, sodium carboxymethyl cellulose, starch, polyhydric alcohols, polyvinyl alcohol (PVA), saccharides, tragacanth gum. The amount of the binder employed may be in the range of from about 0.01 part to 10 parts by weight per 100 parts by weight of the metal powder, and about 0.1 to about 2 parts by weight of the binder is preferably employed.
The alkaline materials may include hydroxides, carbonates, sulfites, thiosulfates, dibasic phosphates, tribasic phosphates, polyphosphates, tri-polyphosphates, or organic acid salts of alkali metals or alkali earth metals. Sodium hydroxide, sodium carbonate sodium sulfite, sodium thiosulfate, tribasic sodium phosphate, dibasic sodium phosphate, potassium hydroxide, potassium carbonate, potassium sulfite, tribasic potassium phosphate, dibasic potassium phosphate, calcium hydroxide, magnesium hydroxide, calcium carbonate, sodium citrate, sodium succinate, sodium propionate and sodium fumarate are preferred; and magnesium hydroxide and sodium thiosulfate are most preferred. The amount of the alkaline material employed may be in the range of about 0.01 part to about 10 parts by weight, preferably about 0.1 part to about 2 parts per 100 parts of the metal powder.
The term "water content" in the specification and the claims means content of free water, and excludes content of water of crystallization. The oxygen absorbent of this invention has less than 1% of free water on the basis of the total weight of the absorbent, preferably less than 0.5% by weight of water, and more preferably less than 0.2% by weight of water.
The oxygen absorbent of this invention is prepared in the following way:
The metal powder is mixed with a solution of the metal halide and optionally the binder and/or the alkaline material, thereby coating the metal halide and optionally the binder and/or the alkaline material on the surface of the metal powder; and the resulting coating is dried until the water content thereof amounts to less than 1% by weight based on the total weight of the absorbent.
The solution of the metal halide may be a conventional aqueous solution thereof. The metal halide may be dissolved in mixture of water and other solvent. The halide concentration may be suitably selected from any concentration up to saturated concentration.
The metal powder is mixed with the solution of the metal halide until the halide is coated on the powder particle.
When the metal powder is coated with the metal halide as well as the binder and/or the alkaline material, the order of the coating is not critical. The metal powder may be coated with these materials simultaneously or successively. The mixing process and the coating process are not critical. Conveniently, the mixture of the metal powder and the solution of the metal halide and other component may be dried as it is, or after the mixture is filtered, the precipitate may be dried.
Preferably the metal powder is mixed with the solution of the metal halide and optionally the binder and/or the alkaline material containing a minor amount of water; and the resulting mixture is dried as it is. The coating is dried until the water content amounts to less than 1%, preferably less than 0.5%, more preferably less than 0.2% and most preferably is substantially zero. When the water content is more than 1%, the resulting absorbent has poor flowability, it is difficult to pack the absorbent, it penetrates through the packaging material and the amount of hydrogen evoluted becomes more.
The drying process is not critical. For example, the coating may be dried under an inert gas atmosphere, one atmospheric pressure or a reduced pressure. In order to shorten the drying time, the metal halide, and optionally the binder and/or the alkaline material are dissolved in the mixture of water and a hydrophilic solvent, such as an alcohol.
The oxygen obsorbent of this invention can be employed under moisture-rich atmosphere, preferably under an atmosphere having a relative humidity of more than 50%. Therefore, it can be profitably employed in a sealed container in which water-containing foodstuffs are packed. In case of packing foodstuffs containing little or no water, the absorbent can be profitably employed with water-containing materials or compounds having water of hydration or crystallization. Also, it can be employed with materials generating water in the packaging system.
The oxygen absorbent of this invention is powder, and the powder absorbent may be employed as it is. Since the moldability of the absorbent is good, the absorbent powder can be tableted by tableting machine. The resulting tablet has good hardness and has the absorbing ability of oxygen as the absorbent powder does.
Since the oxygen absorbent of this invention is prepared by coating the metal halide on the surface of the metal powder, the metal powder and the metal halide contact each other very effectively. Therefore, although the amount of the halide employed is small, the absorbing ability of oxygen is large. Since the amount of the halide employed is small, the absorbent of this invention becomes neither wet nor pasty and, it does not remove a large amount of water from the foodstuff, whereby the degradation of the foodstuff is prevented, and the absorbent neither penetrates into the packaging material nor contaminates the foodstuffs.
Since the oxygen absorbent of this invention has a low water content, it does not absorb oxygen at all even when it is allowed to stand in air. Handling of the absorbent is easy, and little hydrogen is generated in storage or during use of the absorbent.
Only when the oxygen absorbent of this invention is sealed with water-containing foodstuff in a container, it exhibits the absorbing ability of oxygen. Oxygen absorbents having a variety of absorbing properties can be obtained by varying its components and its proportion.
The oxygen absorbent of this invention is practical and has excellent properties.
The present invention is further illustrated by the following Examples and Comparative Examples. However, this invention should not be limited by these examples and comparative examples. The percent and parts in the Examples are based on weight unless otherwise specified.
To 100 gr of Fe powder was added 2 ml. of a 20% aqueous solution of each of the metal halides as given in Table 1, and each of the resulting mixtures was mixed sufficiently and was dried at 40° C. under reduced pressure of 40 mm Hg until its water content amounted substantially to zero. A variety of metal halide-coated metal powders were obtained. Each of the resulting powders in the amount as given in Table 1 was placed in a perforated polyethylene film-laminated paper bag. The bag and sanitary cotton impregnated with 10 ml. of water were placed in a 1l. sealed container so as not to contact the cotton with the bag. The amount of oxygen absorbed was measured at 25° C. periodically. The results are shown in Table 1.
Table 1
______________________________________
Components of oxygen
absorbent Change in amount of oxygen
Fe absorbed with time (ml.)
Run powder metal halide
after after after
No. (gr) kinds mg 20 hrs 40 hrs 80 hrs
______________________________________
1 1 NaCl 4 45 133 155
2 1 NaBr 4 70 107 145
3 1 KI 4 64 99 116
4 1 CaCl.sub.2
4 64 114 158
5 1 KCl 4 45 132 153
6 1 MgCl.sub.2
4 62 112 156
______________________________________
Evolution of a little hydrogen was detected. The hydrogen evolution after 80 hours is given in Table 2.
Table 2 ______________________________________ Run Hydrogen concentration in the sealed No. container after 80 hours passed (%) ______________________________________ 1 0.003 2 0.002 3 0.004 4 0.005 5 0.002 6 0.004 ______________________________________
Stain on the paper due to the penetration of the absorbent into the paper bag was not detected.
One gram of Fe powder was mixed with 4 mg of NaCl powder. The resulting powdery mixture was placed in a perforated polyethylene-film-laminated paper bag. The bag and sanitary cotton impregnated with 10 ml. of water in a 1l. sealed container so as not to contact the cotton with the bag. The amount of oxygen absorbed was measured at 25° C. periodically. The results are shown in Table 3.
Table 3
______________________________________
Number of hours passed
20 40 80
Amount of oxygen absorbed (ml)
1 1 2
______________________________________
The compound absorbed little oxygen.
One gram of Fe powder, 4 mg of NaCl powder and 0.2 ml. of H2 O were mixed. The resulting mixture was placed in a perforated polyethylene film-laminated paper bag. The bag was placed in a 1l. sealed container. The amount of oxygen absorbed was measured at 25° C. periodically. The results are shown in Table 4.
Table 4
______________________________________
Number of hours passed
20 40 80
Amount of oxygen absorbed (ml)
6 10 17
______________________________________
The amount of oxygen absorbed of the compound employed in Comparative Example 2 was less than that of the absorbent of Example 1. The concentration of hydrogen evoluted in the sealed container was 0.32% after 80 hours passed.
The procedure of Comparative Example 2 was repeated except that the amount of NaCl was 1 gr in place of 4 mg. The results are shown in Table 5.
Table 5
______________________________________
Number of hours passed
20 40 80
Amount of oxygen absorbed (ml)
74 112 155
______________________________________
The concentration of hydrogen evoluted in the sealed container was 2.3% after 80 hours passed. The value was more than that in Example 1.
One gram of Fe powder, 1 gram of NaCl powder and 0.2 ml. of H2 O were mixed, and the resulting powdery mixture was placed in a perforated polyethylene film-laminated paper bag. The bag and sanitary cotton imprenated with 10 ml. of water were placed in a 1l. sealed container so as not to contact the cotton with the bag. The absorbing ability of oxygen was measured at 25° C. periodically. The results are shown in Table 6.
Table 6
______________________________________
Number of hours passed
20 40 80
Amount of oxygen absorbed (ml)
63 98 154
______________________________________
The concentration of hydrogen evolved in the sealed container was 3.1%. The amount was much. Stain on the paper not due to the penetration of the compound into the paper was detected two days after the compound was set to absorb oxygen. Black stain on the all portion of paper in contact with the powder was detected in four days.
0.4 gr of NaCl powder, 0.4 gr of each of the binders as given in Table 7 and 40 ml. of water were mixed. To the mixture was added 100 gr. of Fe powder. The resulting mixture was mixed sufficiently and was dried at 80° C. under reduced pressure of 10 mm Hg until its water content amounted substantially to zero. Each of the metal halide-coated metal powders were obtained. Each of the resulting powders in the amount as given in Table 7 was placed in a perforated polyethylene film-laminated paper bag. The bag and sanitary cotton impregnated with 10 ml. of water were placed in a 2l. sealed contained so as not to contact the bag with the cotton. The absorbing amount of oxygen was measured at 25° C. periodically. The results are shown in Table 7.
Table 7
______________________________________
Components of absorbent
Change in amount
and its proportion of oxygen
Fe absorbed with time (ml.)
Run powder NaCl Binder after after after
No. (g) (mg) Kind mg 20 hrs
40 hrs
80 hrs
______________________________________
1 1 4 sodium
2 136 192 238
2 1 4 starch
2 128 185 236
3 1 4 CMC 2 109 166 230
4 1 4 PVA 2 107 176 232
______________________________________
The concentration of hydrogen evolved in the sealed container after 80 hours was given in Table 8.
Table 8 ______________________________________ Run Hydrogen concentration in the sealed container No. after 80 hours passed (%) ______________________________________ 1 0.0002 2 0.0004 3 0.0002 4 0.0003 ______________________________________
It is apparent from Table 8 that little generation of hydrogen was detected. Also stain on the paper was not detected.
To 1 gr of Fe powder was added a various amounts of a 10% aqueous solution of NaCl. The resulting mixture was mixed sufficiently, and dried at 60° C. reduced pressure of 60 mm Hg until its water content amounted substantially to zero. Each of the NaCl-coated Fe powders was obtained as given in Table 9. Each of the resulting powders was placed in a preforated polyethylene film-laminated paper bag. The bag and sanitary cotton impregnated water 10 ml. of water were placed in a 500 ml. sealed container. The container was left to stand at 25° C. The oxygen concentration in the container was measured after 30 hours. As a result, the concentrations all were 0% as shown in Table 9.
Table 9 ______________________________________ No. NaCl conc. O.sub.2 conc. after 30 hrs ______________________________________ 1 1 mg 0% 2 5 0 3 10 0 ______________________________________
To 100 gr of Fe powder was added 50 ml. of a 1% aqueous solution of NaCl, and the resulting mixture was mixed sufficiently and dried at 50° C. under reduced pressure of 20 mm Hg until its water content amounted substantially to zero. The NaCl (0.5 parts)-coated Fe powder (100 parts) was obtained. Two grams of the resulting powder was placed in a perforated polyethylene film-laminated paper bag. The bag and bread were placed in a 500 ml. sealed container. The container was left to stand at 25° C. The oxygen concentration in the container was measured periodically. Results are shown in Table 10.
Table 10
______________________________________
Number of hours passed
10 hrs 20 hrs 30 hrs
30 days
Oxygen concentration %
12.4 3.9 0 0
______________________________________
As a control, only bread was left to stand in a sealed container at 25° C. without applying any oxygen absorbent thereto.
Growing of mold and taste of bread by organoleptic test were observed in Example 4 and control. The taste was evaluated by the following five ratings:
______________________________________ Ratings 5 4 3 2 1 ______________________________________ ##STR1## putrefaction ______________________________________
Whether the test bread gets moldy was evaluated by the following four degree scale.
______________________________________ Ratings ______________________________________ - No mildew grew + Slight mildew grew ++ Mildew grew to a considerable extent +++ A great amount of mildew grew ______________________________________
Table 11
______________________________________
Number Example (oxygen Control (no oxygen
of days
absorbent was used)
absorbent was used)
passed mold taste mold taste
______________________________________
4 -- 5 - 3
8 -- 5 + 1 sour odor
12 -- 4 ++ 1 putrefactive
odor
30 -- 3 +++ 1 putrefactive
odor
______________________________________
To one hundred gr of Fe powder was added 50 ml. of a 0.2% aqueous solution of CaCl2, and the resulting mixture was mixed sufficiently and dried at 40° C. under reduced pressure of 40 mm Hg until its water content amounted substantially to zero. The CaCl2 (0.1 part)-coated Fe powder (100 parts) was obtained. The resulting powder was placed in a perforated polyethylene film-laminated paper bag. The bag and each of the following foodstuffs were placed in a 500 ml. sealed container and left to stand for testing the preservation of the foodstuff. Only one of each of the foodstuffs was lefted to stand in the sealed container as control test.
Growing of mold on the foodstuffs and taste thereof were tested as in Example 4.
Sponge cake (Preservating temperature was 25° C.).
Table 12
______________________________________
Number Example 5 (oxygen
Control (no oxygen
of days
absorbent was used)
absorbent was used)
passed mold taste mold taste
______________________________________
4 -- 5 - 3
8 -- 5 - 2
12 -- 5 + 1
30 -- 5 +++ putrefaction
______________________________________
Table 13
______________________________________
Strawberries (presenting temperature was 5° C)
Example 5 Control
(oxygen absorbent
(no oxygen absorbent
Preservation
was used) was used
days taste taste
______________________________________
first day 5 5
second day 5 3
third day 4 1
fourth day 4 1
______________________________________
Table 14
______________________________________
Sweet broiled chestnuts (25° C)
Example 5 Control
(oxygen absorbent
(no oxygen absorbent
preservation
was used) was used)
days mold taste mold taste
______________________________________
1st day -- 5 - 5
5th day -- 5 - 2
10th day -- 4 ± 2
15th day -- 4 + 1
20th day -- 4 ++ 1
______________________________________
To 100 gr of each of metal powder was added 2 ml. of a 20% aqueous solution of NaCl, and the resulting mixture was mixed sufficiently and dried at 40° C. under reduced pressure of 40 mm Hg until its water content amounted substantially to zero. The NaCl (0.4 parts)-coated metal powders (100 parts) were obtained. The absorbing ability of oxygen was measured by using the resulting powders as in Example 1. The results are shown in Table 15.
Table 15
______________________________________
Components and proportion of
Change in amount of
oxygen absorbent oxygen absorbed with
kinds of time (ml)
metal after after after
powders
g NaCl (mg) 30 hrs 40 hrs 80 hrs
______________________________________
Fe 1 4 45 133 155
Cu 1 4 6 13 28
Zn 1 4 32 53 78
______________________________________
In 100 ml. of water were dissolved 0.6 gr of NaCl and 0.1 gr of each of the alkaline materials as given in Table 15. To the resulting solution was added 100 gr of Fe powder. The resulting mixture was mixed with stirring. The mixture was heated to 100° C. in a nitrogen atmosphere to dry the mixture until its water content amounted substantially to zero.
One gram of each of the resulting metal halide (0.6 parts) and alkaline material (0.1 part)-coated metal powder (100 parts) was placed in a perforated polyethylene film-laminated paper bag. The bag and sanitary cotton impregnated with 10 ml. of water were placed in a 1l. sealed container so as not to contact the bag with the cotton. The container was left to stand at 25° C. The oxygen concentration after 30 hours and the hydrogen concentration after 80 hours were measured. The results are shown in Table 16.
Table 16
______________________________________
Alkaline
Oxygen concentration
Hydrogen concentration
materials
after 30 hrs (%)
after 80 hrs (%)
______________________________________
NaOH 0.1 0.0001
Na.sub.2 SO.sub.3
0.0 0.0002
Na.sub.2 CO.sub.3
0.1 0.0001
KOH 0.0 0.0002
Ca(OH).sub.2
0.0 0.0001
Mg(OH).sub.2
0.0 0.0001
Na.sub.2 S.sub.2 O.sub.3
0.0 0.0001
______________________________________
In 50 ml. of water were dissolved 2 gr of NaCl and 0.5 gr of KOH. To the aqueous solution was added 100 gr of Fe powder. The resulting mixture was mixed with stirring. The powder was filtered by Nutsche to obtain cake. The cake was dried at 60° C. under reduced pressure of 20 mm Hg until its water content amounted substantially to zero. The amounts of NaCl and KOH adhering to the surface of the Fe powder was 0.37% and 0.093%, respectively.
The resulting metal halide-coated metal powder was placed in a perforated polyethylene film-laminated paper bag. The bag and sanitary cotton impregnated with 10 ml. of water were placed in a 1l. sealed container so as not to contact the bag with the cotton. The container was left to stand at 25° C. After 30 hours passed, the oxygen concentration was 0.0%. After 80 hours passed, the hydrogen concentration was 0.0003%.
In 40 ml. of H2 O were dissolved 0.4 gr of NaCl, 0.2 gr of NaOH and 0.4 gr of sodium alginate. To the resulting aqueous solution was added 100 gr of Fe powder with stirring. The resulting mixture was dried at 80° C. under reduced pressure of 40 mm Hg until its water content amounted substantially to zero. One gram of the resulting NaCl-coated metal powder was placed in a perforated polyethylene film-laminated paper bag. The bag and sanitary cotton impregnated with 10 ml. of water were placed in a 1l. sealed container so as not to contact the bag with the cotton. The container was left to stand at 25° C. After 30 hours passed, the oxygen concentration was 0.0%. After 80 hours passed, the hydrogen concentration was 0.0000%.
To 100 gr of Fe powder was added each of the aqueous solutions of NaCl as given in Table 16. After the resulting mixture was mixed, it was dried at 80° C. under reduced pressure of 20 mm Hg until its water content amounted to substantially to zero. One gram of each of the resulting NaCl-coated Fe powder as given in Table 17 was placed in a perforated polyethylene film-laminated paper bag. The bag and sanitary cotton impregnated with 10 ml. of water were placed in a 1l. sealed container so as not to contact the bag with the cotton. The container was lefted to stand at 25° C. The amount of oxygen absorbed was measured periodically. After 80 hours passed, the hydrogen concentration was also measured. The results are shown in Table 17.
Table 17
______________________________________
Concentration of
change in amount
NaCl solution and
of O.sub.2 absorbed with
H.sub.2 concentra-
Run amount of solution
time (hrs) tion after 80
No. added 20 40 80 hours passed
______________________________________
1 0.1% NaCl 10ml 22 61 101 0.001
2 1% NaCl 10ml 35 92 142 0.002
3 20% NaCl 5ml 58 130 153 0.003
4 20% NaCl 25ml 62 126 149 0.005
______________________________________
To 10l. of water was dissolved 0.5 Kg of KCl. To the solution was added 100.0 Kg of Fe powder with stirring. The solution was dried with stirring at 40° C. under reduced pressure of 40 mm Hg when the weight of the solution amounted to 101.0 Kg, the vacuum drying was discontinued. The free flowable KCl (0.5 parts)-coated Fe powder (100 parts) was obtained. One gram of the powder was placed in a perforated polyethylene film-laminated paper bag. The bag and sanitary cotton impregnated with 10 ml. of water were placed in a 1l. sealed container so as not to contact the bag with the cotton. The container was left to stand at 25° C. The amount of oxygen absorbed and the amount of H2 generated was measured periodically. The results are shown in Table 18.
Table 18
______________________________________
Number of hours passed
20 40 80
Amount of O.sub.2 absorbed (ml)
46 135 157
Amount of H.sub.2 generated
-- -- 0.006%
______________________________________
2g Each of the powder could be distributed in said paper bag by automatic filling machine within the tolerance of ± 0.1 gr.
One gram of the powder obtained in Example 11 was placed in a perforated polyethylene film-laminated paper bag. The bag was left to stand for 6 months in a room maintained at a relative humidity of 50-60%. Thereafter, the bag and sanitary cotton impregnated with 10 ml. of water were placed in a 1l. sealed container so as not to contact the bag with the cotton. The amount of oxygen absorbed was measured at 25° C. periodically. The results are shown in Table 19.
Table 19
______________________________________
Number of hours passed
20 40 80
Amount of oxygen absorbed (ml)
43 134 161
______________________________________
The concentration of hydrogen generated after 80 hours was 0.006%.
To 100 gr of Fe powder was added 125 ml. of a 20% aqueous solution of NaCl, and the resulting mixture was mixed sufficiently and dried at 40° C. under reduced pressure of 40 mm Hg until its water content amounted substantially to zero. 1.25 gr of the powder was placed in a perforated polyethylene film-laminated paper bag. The bag and sanitary cotton impregnated with 10 ml. of water was placed in a 1l. sealed container so as not to contact the bag with the cotton. The amount of oxygen absorbed was measured at 25° C. periodically. The results are shown in Table 20.
Table 20
______________________________________
Number of hours passed
20 40 80
Amount of oxygen absorbed (ml)
18 32 45
______________________________________
The amount of oxygen absorbed was lowered in comparison with Example 1.
The resulting powder consisted of the NaCl-coated Fe powder and white NaCl crystal, and had poor flowability. Since the powder is deliquescent, it was impossible to fill paper bags with the powder automatically by automatic filling machine.
To 100.0 Kg of Fe powder was added 2.0 Kg of a 20 aqueous solution of NaCl, and the resulting mixture was mixed sufficiently and dried at 40° C. under reduced pressure of 40 mm Hg. When the weight of the mixture amounted to 102.5 kg, the vacuum drying was discontinued. Since the resulting composition contained 2% of water, it had poor flowability. When attempts were made to automatically fill paper bags with the powder by automatic filling machine, it was not possible to do so, because it clogged into the measuring parts of the machine. One gram of the powder was placed in a perforated polyethylene film-laminated paper bag. The bag and sanitary cotton impregnated with 10 ml. of water were placed in a 1l. sealed container. The amount of oxygen absorbed was measured at 25° C. periodically. The results are shown in Table 21.
Table 21
______________________________________
Number of hours passed
20 40 80
Amount of oxygen absorbed (ml)
26 43 65
______________________________________
The values were less than those in Example 1.
Claims (54)
1. An oxygen absorbent in which at least one metal halide is coated on the surface of at least one metal powder, the amount of metal halide coated being in the range of from about 0.001 to about 10 parts by weight per 100 parts by weight of the metal powder, the water content of the absorbent being less than 1% by weight based on the basis of total weight of the absorbent.
2. The oxygen absorbent as defined in claim 1 wherein the metal powder is selected from the group consisting of iron powder, zinc powder, copper powder and mixture thereof.
3. The oxygen absorbent as defined in claim 2 wherein the metal powder is iron powder.
4. The oxygen absorbent as defined in claim 1 wherein the metal constituting the metal halide is selected from lithium, sodium, potassium, magnesium, calcium and barium.
5. The oxygen absorbent as defined in claim 1 wherein the halide constituting the metal halide is selected from the group consisting of chloride, bromide and iodide.
6. The oxygen absorbent as defined in claim 5 wherein the halide is chloride.
7. The oxygen absorbent as defined in claim 1 wherein the amount of the metal halide coated is in the range of from about 0.01 to about 5 parts by weight per 100 parts by weight of the metal powder.
8. The oxygen absorbent as defined in claim 1 wherein the water content is less than 0.5% by weight on the basis of total weight of the absorbent.
9. The oxygen absorbent as defined in claim 1 wherein the water content is less than 0.2% by weight on the basis of total weight of the absorbent.
10. An oxygen absorbent in which at least one metal halide and at least one binder and/or at least one alkaline material are coated on the surface of at least one metal powder, the amount of the metal halide coated being in the range of from about 0.001 to about 10 parts by weight per 100 parts by weight of the metal powder, the water content of the absorbent being less than 1% by weight on the basis of total weight of the absorbent.
11. The oxygen absorbent as defined in claim 10 wherein the metal powder is selected from the group consisting of iron powder, zinc powder, copper powder and mixture thereof.
12. The oxygen absorbent as defined in claim 11 wherein the metal powder is iron powder.
13. The oxygen absorbent as defined in claim 10 wherein the metal constituting the metal halide is selected from lithium, sodium, potassium, magnesium, calcium and barium.
14. The oxygen absorbent as defined in claim 10 wherein the halide constituting the metal halide is selected from the group consisting of chloride, bromide and iodide.
15. The oxygen absorbent as defined in claim 14 wherein the halide is chloride.
16. The oxygen absorbent as defined in claim 10 wherein the amount of the metal halide coated is in the range of from about 0.01 to about 5 parts by weight per 100 parts by weight of the metal powder.
17. The oxygen absorbent as defined in claim 10 wherein the water content is less than 0.5% by weight on the basis of total weight of the absorbent.
18. The oxygen absorbent as defined in claim 10 wherein the water content is less than 0.2% by weight on the basis of total weight of the absorbent.
19. The oxygen absorbent as defined in claim 10 wherein the binder is water soluble polymer.
20. The oxygen absorbent as defined in claim 19 wherein the water soluble polymer is selected from the group consisting of sodium alginate, carboxymethyl cellulose, hydroxymethyl cellulose, methyl cellulose, ethyl cellulose, propyl cellulose, sodium carboxymethyl cellulose, starch, polyhydric alcohols, polyvinyl alcohol, saccharides and tragacanth gum.
21. The oxygen absorbent as defined in claim 10 wherein the amount of the binder coated is in the range of from about 0.01 part to about 10 parts by weight per 100 parts by weight of the metal powder.
22. The oxygen absorbent as defined in claim 10 wherein the alkaline material is selected from the group consisting of hydroxides, carbonates, sulfites, thiosulfates, dibasic phosphates, tribasic phosphates, polyphosphates, tripolyphosphates and organic acid salts of alkali metals or alkali earth metals.
23. The oxygen absorbent as defined in claim 10 wherein the alkaline material is magnesium hydroxide.
24. The oxygen absorbent as defined in claim 10 wherein the alkaline material is sodium thiosulfate.
25. The oxygen absorbent as defined in claim 10 wherein the amount of the alkaline material coated is in the range of from about 0.01 part to about 10 parts by weight per 100 parts by weight of the metal powder.
26. The oxygen absorbent as defined in claim 10 wherein the amount of the alkaline material coated is in the range of from about 0.1 part to about 2 parts by weight per 100 parts by weight of the metal powder.
27. A process for producing an oxygen absorbent, characterized by mixing at least one metal powder with a solution of at least one metal halide to coat metal halide on the surface of the metal powder, the amount of the metal halide coated being in the range of from about 0.001 part to about 10 parts by weight per 100 parts by weight of the metal powder, and then drying the coating until its water content amounts to less than 1% by weight on the basis of total weight of the absorbent.
28. The process as defined in claim 27 wherein the metal powder is selected from the group consisting of iron powder, zinc powder, copper powder and mixture thereof.
29. The process as defined in claim 28 wherein the metal powder is iron powder.
30. The process as defined in claim 27 wherein the metal constituting the metal halide is selected from lithium, sodium, potassium, magnesium, calcium and barium.
31. The process as defined in claim 27 wherein the halide constituting the metal halide is selected from the group consisting of chloride, bromide and iodide.
32. The process as defined in claim 31 wherein the halide is chloride.
33. The process as defined in claim 27 wherein the amount of the metal halide coated is in the range of from about 0.01 to about 5 parts by weight per 100 parts by weight of the metal powder.
34. The process as defined in claim 27 wherein the solution of the metal halide is aqueous solution.
35. The process as defined in claim 27 wherein the water content is less than 0.5% by weight on the basis of total weight of the absorbent.
36. The process as defined in claim 27 wherein the water content is less than 0.2% by weight on the basis of total weight of the absorbent.
37. A process for producing an oxygen absorbent, characterized by mixing at least one metal powder with at least one metal halide solution and at least binder and/or at least one alkaline material to coat the metal halide and the binder and/or the alkaline material on the surface of the metal powder, the amount of the metal halide coated being in the range of from about 0.001 part to about 10 parts by weight per 100 parts by weight of the metal powder, and then drying the coating until its water content amounts to less than 1% by weight on the basis of total weight of the absorbent.
38. The process as defined in claim 37 wherein the metal powder is selected from the group consisting of iron powder, zinc powder, copper powder and mixture thereof.
39. The process as defined in claim 38 wherein the metal powder is iron powder.
40. The process as defined in claim 37 wherein the metal constituting the metal halide is selected from lithium, sodium, potassium, magnesium, calcium and barium.
41. The process as defined in claim 37 wherein the halide constituting the metal halide is selected from the group consisting of chloride, bromide and iodide.
42. The process as defined in claim 41 wherein the halide is chloride.
43. The process as defined in claim 37 wherein the amount of the metal halide coated is in the range of from about 0.01 to about 5 parts by weight per 100 parts by weight of the metal powder.
44. The process as defined in claim 37 wherein the metal halide solution is aqueous solution.
45. The process as defined in claim 37 wherein the water content is less than 0.5% by weight on the basis of total weight of the absorbent.
46. The process as defined in claim 37 wherein the water content is less than 0.2% by weight on the basis of total weight of the absorbent.
47. The process as defined in claim 37 wherein the binder is water soluble polymer.
48. The process as defined in claim 37 wherein the water soluble polymer is selected from the group consisting of sodium alginate, carboxymethyl cellulose, hydroxymethyl cellulose, methyl cellulose, ethyl cellulose, propyl cellulose, sodium carboxymethyl cellulose, starch, polyhydric alcohols, polyvinyl alcohol, saccharides and tragacanth gum.
49. The process as defined in claim 37 wherein the amount of the binder coated is in the range of from about 0.01 part to about 10 parts by weight per 100 parts by weight of the metal powder.
50. The process as defined in claim 37 wherein the alkaline material is selected from the group consisting of hydroxides, carbonates, sulfites thiosulfates, dibasic phosphates, tribasic phosphates, polyphosphates, tripolyphosphates or organic acid salts of alkali metals or alkali earth metals.
51. The process as defined in claim 37 wherein the alkaline material is magnesium hydroxide.
52. The process as defined in claim 37 wherein the alkaline material is sodium thiosulfate.
53. The process as defined in claim 37 wherein the amount of the alkaline material coated is in the range of from about 0.01 part to about 10 parts by weight per 100 parts by weight of the metal powder.
54. The process as defined in claim 37 wherein the amount of the alkaline material coated is in the range of from about 0.1 part to about 2 parts by weight per 100 parts by weight of the metal powder.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8416976A JPS5314185A (en) | 1976-07-15 | 1976-07-15 | Production of oxygen absorbent |
| JP51-84169 | 1976-07-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4127503A true US4127503A (en) | 1978-11-28 |
Family
ID=13822984
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US05/816,134 Expired - Lifetime US4127503A (en) | 1976-07-15 | 1977-07-15 | Oxygen absorbent |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US4127503A (en) |
| JP (1) | JPS5314185A (en) |
Cited By (53)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4192773A (en) * | 1977-08-24 | 1980-03-11 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorbent |
| EP0036575A2 (en) * | 1980-03-17 | 1981-09-30 | Mitsubishi Gas Chemical Company, Inc. | A method for storing roasted coffee or beans |
| US4332845A (en) * | 1979-12-21 | 1982-06-01 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorbent-containing bag |
| US4421235A (en) * | 1979-02-08 | 1983-12-20 | Mitsubishi Gas Chemical Co. Inc. | Oxygen absorbent-containing bag and container sealing member having the same |
| US4485133A (en) * | 1981-05-07 | 1984-11-27 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorbent packaging |
| US4487791A (en) * | 1981-05-12 | 1984-12-11 | Mitsubishi Gas Chemical Co., Inc. | Oxygen absorbent packaging |
| US4567157A (en) * | 1982-05-17 | 1986-01-28 | The Dow Chemical Company | Production of phenols and catalyst therefor |
| US4769175A (en) * | 1985-06-26 | 1988-09-06 | Mitsubishi Gas Chemical Company, Inc. | Sheet-like, oxygen-scavenging agent |
| US4786415A (en) * | 1984-04-02 | 1988-11-22 | Daicel Chemical Industries, Ltd. | Separation agent comprising aliphatic ester of polysaccharide |
| US4820442A (en) * | 1985-12-26 | 1989-04-11 | Freund Industrial Co., Ltd. | Preservative composition |
| US4840280A (en) * | 1988-01-28 | 1989-06-20 | American Air Liquide | Sealing cap for liquid food or beverage containers |
| US4914076A (en) * | 1987-12-12 | 1990-04-03 | Kansai Netsukagaku Kabushiki Kaisha | Method of producing an adsorbent for separation and recovery of CO |
| US4992410A (en) * | 1989-02-17 | 1991-02-12 | Multiform Desiccants, Inc. | Oxygen-absorbing package, composition and method of formulation thereof |
| US4996068A (en) * | 1987-12-02 | 1991-02-26 | Mitsubishi Gas Chemical Company | Methods for treating food and a deoxodizer package in a microwave oven |
| US5021515A (en) * | 1987-07-27 | 1991-06-04 | Cmb Foodcan Plc | Packaging |
| US5180518A (en) * | 1989-04-25 | 1993-01-19 | Mitsubishi Gas Chemical Co., Inc. | Oxygen absorbent |
| US5192444A (en) * | 1984-04-02 | 1993-03-09 | Daicel Chemical Industries, Ltd. | Separating with an agent comprising an aliphatic ester of a polysaccharide |
| US5194478A (en) * | 1988-07-11 | 1993-03-16 | A/S Haustrup Plastic | Polymer composition for scavenging oxygen |
| US5207943A (en) * | 1991-01-07 | 1993-05-04 | Multiform Desiccants, Inc. | Oxygen absorber for low moisture products |
| EP0547761A1 (en) * | 1991-11-13 | 1993-06-23 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorber and method for producing same |
| US5241149A (en) * | 1990-10-15 | 1993-08-31 | Mitsubishi Gas Chemical Company, Inc. | Food packing body for heat and microwave treatment |
| US5268098A (en) * | 1984-04-02 | 1993-12-07 | Daicel Chemical Industries, Ltd. | Separation agent comprising aliphatic or aromatic ester of polysaccharide |
| WO1993024221A1 (en) * | 1992-05-26 | 1993-12-09 | Multiform Desiccants, Inc. | Oxygen absorber |
| US5639815A (en) * | 1987-07-27 | 1997-06-17 | Carnaudmetalbox Plc | Packaging |
| EP0787764A2 (en) * | 1996-02-03 | 1997-08-06 | Mitsubishi Gas Chemical Company, Inc. | Oxygen-absorbing resin composition and packing material, multi-layered packing material, package and packing method using the same |
| US5663223A (en) * | 1994-08-11 | 1997-09-02 | Zapata Technologies, Inc. | Flavor protectant closure liner compositions |
| US5667863A (en) * | 1991-01-07 | 1997-09-16 | Multisorb Technologies, Inc. | Oxygen-absorbing label |
| US5686161A (en) * | 1991-01-07 | 1997-11-11 | Multisorb Technologies, Inc. | Moisture-sensitive label |
| EP0864630A1 (en) * | 1997-03-13 | 1998-09-16 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorbing composition, oxygen absorber packet and preservation method |
| US5811142A (en) * | 1996-04-03 | 1998-09-22 | Tenneo Packaging | Modified atmosphere package for cut of raw meat |
| WO1999028411A1 (en) * | 1997-12-02 | 1999-06-10 | Alutech Ltd. | Oxygen-scavenging compositions |
| US5928560A (en) * | 1996-08-08 | 1999-07-27 | Tenneco Packaging Inc. | Oxygen scavenger accelerator |
| US6054153A (en) * | 1998-04-03 | 2000-04-25 | Tenneco Packaging Inc. | Modified atmosphere package with accelerated reduction of oxygen level in meat compartment |
| US6133361A (en) * | 1996-02-03 | 2000-10-17 | Mitsubishi Gas Chemical Company, Inc. | Oxygen-absorbing composition, oxygen-absorbing resin composition, packing material, multi-layered packing, oxygen absorber packet, packing method and preservation method |
| US6139935A (en) * | 1991-01-07 | 2000-10-31 | Multisorb Technologies, Inc. | Oxygen-absorbing label |
| US6209289B1 (en) | 1992-01-30 | 2001-04-03 | Multisorb Technologies, Inc. | Composition for and method of absorbing oxygen in an oxygen/carbon dioxide environment |
| WO2001025369A1 (en) * | 1999-10-01 | 2001-04-12 | Pactiv Corporation | Rapid oxygen absorption by using activators |
| US6231905B1 (en) | 1998-10-08 | 2001-05-15 | Delduca Gary R. | System and method of making a modified atmosphere package comprising an activated oxygen scavenger for packaging meat |
| US6248690B1 (en) | 1992-05-26 | 2001-06-19 | Multisorb Technologies, Inc. | Oxygen absorber |
| US6321509B1 (en) | 1999-06-11 | 2001-11-27 | Pactiv Corporation | Method and apparatus for inserting an oxygen scavenger into a modified atmosphere package |
| US6395195B1 (en) | 1996-08-08 | 2002-05-28 | Pactiv Corporation | Oxygen scavenger accelerator |
| US6926846B1 (en) | 1996-08-08 | 2005-08-09 | Pactiv Corporation | Methods of using an oxygen scavenger |
| WO2006015982A2 (en) * | 2004-08-13 | 2006-02-16 | M & G Polimeri Italia S.P.A. | Method of making vapour deposited oxygen-scavenging particles |
| EP1640408A1 (en) | 2004-09-27 | 2006-03-29 | Futura Polyesters Limited | Oxygen scavenging composition |
| US20080003388A1 (en) * | 2006-05-25 | 2008-01-03 | Graham Packaging Company, L.P. | Multilayer barrier container wall |
| US8277892B2 (en) | 2006-02-25 | 2012-10-02 | Multisorb Technologies, Inc. | Process for creating an oxygen scavenging particle |
| CN102958601A (en) * | 2011-06-09 | 2013-03-06 | 三菱瓦斯化学株式会社 | Deoxidant composition, and deoxidizing packaging material and method for deoxidizing using same |
| CN103154609A (en) * | 2010-09-28 | 2013-06-12 | 皇家飞利浦电子股份有限公司 | Light-emitting arrangement |
| US20140076173A1 (en) * | 2012-04-05 | 2014-03-20 | Anheuser-Busch, Llc | Systems for introducing flavor to a non-carbonated base liquid |
| CN104415658A (en) * | 2013-09-10 | 2015-03-18 | 湖南华望熏蒸消毒有限公司 | Chemical gas regulating agent and preparation method thereof |
| WO2017048321A1 (en) | 2015-09-15 | 2017-03-23 | Boveda, Inc. | Devices and methods for controlling headspace humidity and oxygen levels |
| US10220992B2 (en) | 2016-10-12 | 2019-03-05 | Drug Plastics & Glass Company, Inc. | Container assembly and closure with predetermined humidity and related method |
| US11612936B2 (en) * | 2020-02-24 | 2023-03-28 | University Of Science And Technology Beijing | Method for preparing oxygen-free passivated titanium or titanium-alloy powder product by means of gas-solid fluidization |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54128995A (en) * | 1978-03-31 | 1979-10-05 | Teijin Ltd | Oxygen capturing composition |
| JPS5549250A (en) * | 1978-10-02 | 1980-04-09 | Tokai Rubber Ind Ltd | Duct for circulating gasoline |
| JPS5878554A (en) * | 1981-11-04 | 1983-05-12 | Mitsubishi Gas Chem Co Inc | Preservation of cut raw rice cake |
| JPS60150752A (en) * | 1984-08-20 | 1985-08-08 | テルモ株式会社 | Fungicidal method of medical instrument |
| JPS6430316A (en) * | 1987-07-27 | 1989-02-01 | Matsushita Electric Ind Co Ltd | Balance-to-unbalance transformer |
| CN1212814C (en) * | 1996-07-02 | 2005-08-03 | 日本巴伊欧尼克斯股份有限公司 | Sheet-shaped heating element and method for manufacturing same |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB553991A (en) | 1941-12-03 | 1943-06-15 | Frederick Arthur Isherwood | Improved method of storing foodstuffs or other products in sealed containers |
| US2825651A (en) * | 1957-07-01 | 1958-03-04 | Carnation Co | In-package oxygen remover |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB226512A (en) * | 1923-12-21 | 1925-05-21 | Vickers Electrical Co Ltd | Improved means for deoxidising gases containing oxygen |
| DE869042C (en) * | 1950-04-15 | 1953-03-02 | Bayer Ag | Process for the absorption of oxygen |
| DE1109499B (en) * | 1957-10-19 | 1961-06-22 | Norbert Buchner | Oxygen removal from food packages under protective gas or under vacuum |
| JPS5121982A (en) * | 1974-08-14 | 1976-02-21 | Keiji Taniuchi | Kan niokeru hikichigirishikikaikohenno keiseihoho |
-
1976
- 1976-07-15 JP JP8416976A patent/JPS5314185A/en active Granted
-
1977
- 1977-07-15 US US05/816,134 patent/US4127503A/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB553991A (en) | 1941-12-03 | 1943-06-15 | Frederick Arthur Isherwood | Improved method of storing foodstuffs or other products in sealed containers |
| US2825651A (en) * | 1957-07-01 | 1958-03-04 | Carnation Co | In-package oxygen remover |
Cited By (105)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4192773A (en) * | 1977-08-24 | 1980-03-11 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorbent |
| US4421235A (en) * | 1979-02-08 | 1983-12-20 | Mitsubishi Gas Chemical Co. Inc. | Oxygen absorbent-containing bag and container sealing member having the same |
| US4332845A (en) * | 1979-12-21 | 1982-06-01 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorbent-containing bag |
| EP0036575A2 (en) * | 1980-03-17 | 1981-09-30 | Mitsubishi Gas Chemical Company, Inc. | A method for storing roasted coffee or beans |
| US4366179A (en) * | 1980-03-17 | 1982-12-28 | Mitsubishi Gas Chemical Company, Inc. | Oxygen and carbon dioxide absorbent and process for storing coffee by using the same |
| EP0036575A3 (en) * | 1980-03-17 | 1983-03-16 | Mitsubishi Gas Chemical Company, Inc. | Oxygen and carbon dioxide absorbent and process for storing coffee by using the same |
| US4485133A (en) * | 1981-05-07 | 1984-11-27 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorbent packaging |
| US4487791A (en) * | 1981-05-12 | 1984-12-11 | Mitsubishi Gas Chemical Co., Inc. | Oxygen absorbent packaging |
| US4567157A (en) * | 1982-05-17 | 1986-01-28 | The Dow Chemical Company | Production of phenols and catalyst therefor |
| US5472599A (en) * | 1984-04-02 | 1995-12-05 | Daicel Chemical Industries, Ltd. | Separation agent comprising aliphatic or aromatic ester of polysaccharide |
| US5089138A (en) * | 1984-04-02 | 1992-02-18 | Daicel Chemical Industries, Ltd. | Separating with an agent comprising an aliphatic ester of a polysaccharide |
| US4786415A (en) * | 1984-04-02 | 1988-11-22 | Daicel Chemical Industries, Ltd. | Separation agent comprising aliphatic ester of polysaccharide |
| US5334311A (en) * | 1984-04-02 | 1994-08-02 | Daicel Chemical Industries, Ltd. | Separation agent comprising aliphatic or aromatic ester of polysaccharide |
| US4892659A (en) * | 1984-04-02 | 1990-01-09 | Daicel Chemical Industries, Ltd. | Separation agent comprising aliphatic ester of polysaccharide |
| US5415769A (en) * | 1984-04-02 | 1995-05-16 | Daicel Chemical Industries, Ltd. | Separation agent comprising aliphatic or aromatic ester of polysaccharide |
| US5192444A (en) * | 1984-04-02 | 1993-03-09 | Daicel Chemical Industries, Ltd. | Separating with an agent comprising an aliphatic ester of a polysaccharide |
| US5268098A (en) * | 1984-04-02 | 1993-12-07 | Daicel Chemical Industries, Ltd. | Separation agent comprising aliphatic or aromatic ester of polysaccharide |
| US5041226A (en) * | 1984-04-02 | 1991-08-20 | Daicel Chemical Industries, Ltd. | Separating with an agent comprising aliphatic ester of polysaccharide |
| US4769175A (en) * | 1985-06-26 | 1988-09-06 | Mitsubishi Gas Chemical Company, Inc. | Sheet-like, oxygen-scavenging agent |
| US4820442A (en) * | 1985-12-26 | 1989-04-11 | Freund Industrial Co., Ltd. | Preservative composition |
| US5021515A (en) * | 1987-07-27 | 1991-06-04 | Cmb Foodcan Plc | Packaging |
| US5955527A (en) * | 1987-07-27 | 1999-09-21 | Carnaudmetalbox Plc | Packaging |
| US5639815A (en) * | 1987-07-27 | 1997-06-17 | Carnaudmetalbox Plc | Packaging |
| US20050179002A1 (en) * | 1987-07-27 | 2005-08-18 | Constar International, Inc. | Packaging |
| US20040219320A1 (en) * | 1987-07-27 | 2004-11-04 | Constar International, Inc. | Packaging |
| US4996068A (en) * | 1987-12-02 | 1991-02-26 | Mitsubishi Gas Chemical Company | Methods for treating food and a deoxodizer package in a microwave oven |
| US4914076A (en) * | 1987-12-12 | 1990-04-03 | Kansai Netsukagaku Kabushiki Kaisha | Method of producing an adsorbent for separation and recovery of CO |
| US4840280A (en) * | 1988-01-28 | 1989-06-20 | American Air Liquide | Sealing cap for liquid food or beverage containers |
| US5194478A (en) * | 1988-07-11 | 1993-03-16 | A/S Haustrup Plastic | Polymer composition for scavenging oxygen |
| US4992410A (en) * | 1989-02-17 | 1991-02-12 | Multiform Desiccants, Inc. | Oxygen-absorbing package, composition and method of formulation thereof |
| US5180518A (en) * | 1989-04-25 | 1993-01-19 | Mitsubishi Gas Chemical Co., Inc. | Oxygen absorbent |
| US5241149A (en) * | 1990-10-15 | 1993-08-31 | Mitsubishi Gas Chemical Company, Inc. | Food packing body for heat and microwave treatment |
| EP0567529B2 (en) † | 1991-01-07 | 2009-12-02 | Multisorb Technologies, Inc. | Oxygen-absorbing label |
| US5207943A (en) * | 1991-01-07 | 1993-05-04 | Multiform Desiccants, Inc. | Oxygen absorber for low moisture products |
| US6139935A (en) * | 1991-01-07 | 2000-10-31 | Multisorb Technologies, Inc. | Oxygen-absorbing label |
| US5667863A (en) * | 1991-01-07 | 1997-09-16 | Multisorb Technologies, Inc. | Oxygen-absorbing label |
| US5686161A (en) * | 1991-01-07 | 1997-11-11 | Multisorb Technologies, Inc. | Moisture-sensitive label |
| EP0547761A1 (en) * | 1991-11-13 | 1993-06-23 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorber and method for producing same |
| US5725795A (en) * | 1991-11-13 | 1998-03-10 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorber and method for producing same |
| AU667323B2 (en) * | 1991-11-13 | 1996-03-21 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorber and method for producing same |
| US6209289B1 (en) | 1992-01-30 | 2001-04-03 | Multisorb Technologies, Inc. | Composition for and method of absorbing oxygen in an oxygen/carbon dioxide environment |
| US6667273B1 (en) | 1992-01-30 | 2003-12-23 | Multisorb Technologies, Inc. | Composition for absorbing oxygen in an oxygen/carbon dioxide environment |
| US20040087442A1 (en) * | 1992-01-30 | 2004-05-06 | Multisorb Technologies, Inc. | Composition for absorbing oxygen in an oxygen/carbon dioxide environment |
| US6248690B1 (en) | 1992-05-26 | 2001-06-19 | Multisorb Technologies, Inc. | Oxygen absorber |
| US6436872B2 (en) | 1992-05-26 | 2002-08-20 | Multisorb Technologies, Inc. | Oxygen absorber |
| WO1993024221A1 (en) * | 1992-05-26 | 1993-12-09 | Multiform Desiccants, Inc. | Oxygen absorber |
| US5663223A (en) * | 1994-08-11 | 1997-09-02 | Zapata Technologies, Inc. | Flavor protectant closure liner compositions |
| USRE36815E (en) * | 1994-08-11 | 2000-08-08 | Zapata Technologies, Inc. | Flavor protectant closure liner compositions |
| US5863964A (en) * | 1994-08-11 | 1999-01-26 | Zapata Technologies, Inc. | Flavor protectant closure liner compositions |
| EP0787764A3 (en) * | 1996-02-03 | 1998-11-18 | Mitsubishi Gas Chemical Company, Inc. | Oxygen-absorbing resin composition and packing material, multi-layered packing material, package and packing method using the same |
| US6133361A (en) * | 1996-02-03 | 2000-10-17 | Mitsubishi Gas Chemical Company, Inc. | Oxygen-absorbing composition, oxygen-absorbing resin composition, packing material, multi-layered packing, oxygen absorber packet, packing method and preservation method |
| EP0787764A2 (en) * | 1996-02-03 | 1997-08-06 | Mitsubishi Gas Chemical Company, Inc. | Oxygen-absorbing resin composition and packing material, multi-layered packing material, package and packing method using the same |
| US5889093A (en) * | 1996-02-03 | 1999-03-30 | Mitsubishi Gas Chemical Company, Inc. | Oxygen-absorbing resin composition and packing material, multi-layered packing material, package and packing method using the same |
| US5948457A (en) * | 1996-04-03 | 1999-09-07 | Tenneco Packaging Inc. | Modified atmosphere package |
| US5811142A (en) * | 1996-04-03 | 1998-09-22 | Tenneo Packaging | Modified atmosphere package for cut of raw meat |
| US6183790B1 (en) | 1996-04-03 | 2001-02-06 | Pactiv Corporation | Modified atmosphere package |
| US6508955B1 (en) | 1996-08-08 | 2003-01-21 | Pactiv Corporation | Oxygen scavenger accelerator |
| US7147799B2 (en) | 1996-08-08 | 2006-12-12 | Pactiv Corporation | Methods of using an oxygen scavenger |
| US6395195B1 (en) | 1996-08-08 | 2002-05-28 | Pactiv Corporation | Oxygen scavenger accelerator |
| US6315921B1 (en) | 1996-08-08 | 2001-11-13 | Pactiv Corporation | Oxygen scavenger accelerator |
| US5928560A (en) * | 1996-08-08 | 1999-07-27 | Tenneco Packaging Inc. | Oxygen scavenger accelerator |
| US6926846B1 (en) | 1996-08-08 | 2005-08-09 | Pactiv Corporation | Methods of using an oxygen scavenger |
| US6666988B2 (en) | 1996-08-08 | 2003-12-23 | Pactiv Corporation | Methods of using an oxygen scavenger |
| EP0864630A1 (en) * | 1997-03-13 | 1998-09-16 | Mitsubishi Gas Chemical Company, Inc. | Oxygen absorbing composition, oxygen absorber packet and preservation method |
| WO1999028411A1 (en) * | 1997-12-02 | 1999-06-10 | Alutech Ltd. | Oxygen-scavenging compositions |
| US6054153A (en) * | 1998-04-03 | 2000-04-25 | Tenneco Packaging Inc. | Modified atmosphere package with accelerated reduction of oxygen level in meat compartment |
| US6132781A (en) * | 1998-04-03 | 2000-10-17 | Pactiv Corporation | Modified atmosphere package with accelerated reduction of oxygen level in meat compartment |
| US6231905B1 (en) | 1998-10-08 | 2001-05-15 | Delduca Gary R. | System and method of making a modified atmosphere package comprising an activated oxygen scavenger for packaging meat |
| US6494023B2 (en) | 1999-06-11 | 2002-12-17 | Pactiv Corporation | Apparatus for inserting an oxygen scavenger into a modified atmosphere package |
| US6321509B1 (en) | 1999-06-11 | 2001-11-27 | Pactiv Corporation | Method and apparatus for inserting an oxygen scavenger into a modified atmosphere package |
| US6616861B1 (en) | 1999-10-01 | 2003-09-09 | Pactiv Corporation | Rapid oxygen absorption by using activators |
| WO2001025369A1 (en) * | 1999-10-01 | 2001-04-12 | Pactiv Corporation | Rapid oxygen absorption by using activators |
| WO2006015982A3 (en) * | 2004-08-13 | 2006-07-06 | M & G Polimeri Italia Spa | Method of making vapour deposited oxygen-scavenging particles |
| US20100068379A1 (en) * | 2004-08-13 | 2010-03-18 | Rollick Kevin L | Method of Making Vapor Deposited Oxygen-Scavenging Particles |
| US20060033078A1 (en) * | 2004-08-13 | 2006-02-16 | Rollick Kevin L | Method of making vapour deposited oxygen-scavenging particles |
| KR101231503B1 (en) * | 2004-08-13 | 2013-02-08 | 멀티서브 테크놀로지스 인코포레이티드 | Method of making vapour deposited oxygen-scavenging particles |
| US7622153B2 (en) | 2004-08-13 | 2009-11-24 | M&G Usa Corporation | Method of making vapour deposited oxygen-scavenging particles |
| WO2006015982A2 (en) * | 2004-08-13 | 2006-02-16 | M & G Polimeri Italia S.P.A. | Method of making vapour deposited oxygen-scavenging particles |
| AU2005271158B2 (en) * | 2004-08-13 | 2009-12-03 | Multisorb Technologies, Inc. | Method of making vapour deposited oxygen-scavenging particles |
| AU2009233623B2 (en) * | 2004-08-13 | 2011-03-24 | Multisorb Technologies, Inc. | Method of making vapour deposited oxygen-scavenging particles |
| US7781018B2 (en) * | 2004-08-13 | 2010-08-24 | M&G Usa Corporation | Method of making vapor deposited oxygen-scavenging particles |
| EP1640408A1 (en) | 2004-09-27 | 2006-03-29 | Futura Polyesters Limited | Oxygen scavenging composition |
| US8277892B2 (en) | 2006-02-25 | 2012-10-02 | Multisorb Technologies, Inc. | Process for creating an oxygen scavenging particle |
| US20080003388A1 (en) * | 2006-05-25 | 2008-01-03 | Graham Packaging Company, L.P. | Multilayer barrier container wall |
| CN103154609B (en) * | 2010-09-28 | 2016-06-29 | 皇家飞利浦电子股份有限公司 | Light-emitting device |
| CN103154609A (en) * | 2010-09-28 | 2013-06-12 | 皇家飞利浦电子股份有限公司 | Light-emitting arrangement |
| US9161396B2 (en) * | 2010-09-28 | 2015-10-13 | Koninklijke Philips N.V. | Light-emitting arrangement |
| US20130175920A1 (en) * | 2010-09-28 | 2013-07-11 | Koninklijk Philips Electronics N.V. | Light-emitting arrangement |
| KR20140043922A (en) * | 2011-06-09 | 2014-04-11 | 미츠비시 가스 가가쿠 가부시키가이샤 | Deoxidant composition, and deoxidizing packaging material and method for deoxidizing using same |
| EP2719453B1 (en) * | 2011-06-09 | 2018-04-25 | Mitsubishi Gas Chemical Company, Inc. | Deoxidant composition, and deoxidizing packaging material and method for deoxidizing using same |
| CN102958601B (en) * | 2011-06-09 | 2015-02-18 | 三菱瓦斯化学株式会社 | Deoxidant composition, and deoxidizing packaging material and method for deoxidizing using same |
| CN102958601A (en) * | 2011-06-09 | 2013-03-06 | 三菱瓦斯化学株式会社 | Deoxidant composition, and deoxidizing packaging material and method for deoxidizing using same |
| US9028712B2 (en) * | 2011-06-09 | 2015-05-12 | Mitsubishi Gas Chemical Company, Inc. | Oxygen scavenger composition, and oxygen scavenger package using the same, and method for oxygen scavenging |
| US20130153827A1 (en) * | 2011-06-09 | 2013-06-20 | Mitsubishi Gas Chemical Company, Inc. | Oxygen scavenger composition, and oxygen scavenger package using the same, and method for oxygen scavenging |
| US20140076173A1 (en) * | 2012-04-05 | 2014-03-20 | Anheuser-Busch, Llc | Systems for introducing flavor to a non-carbonated base liquid |
| US10280388B2 (en) | 2012-04-05 | 2019-05-07 | Anheuser-Busch, Llc | Systems and methods for customized fermented beverages |
| CN104415658A (en) * | 2013-09-10 | 2015-03-18 | 湖南华望熏蒸消毒有限公司 | Chemical gas regulating agent and preparation method thereof |
| WO2017048321A1 (en) | 2015-09-15 | 2017-03-23 | Boveda, Inc. | Devices and methods for controlling headspace humidity and oxygen levels |
| US9750811B2 (en) | 2015-09-15 | 2017-09-05 | Boveda, Inc. | Devices and methods for controlling headspace humidity and oxygen levels |
| US10201612B2 (en) | 2015-09-15 | 2019-02-12 | Boveda, Inc. | Devices and methods for controlling headspace humidity and oxygen levels |
| EP3736042A1 (en) | 2015-09-15 | 2020-11-11 | Boveda, Inc. | Devices and methods for controlling headspace humidity and oxygen levels |
| US10220992B2 (en) | 2016-10-12 | 2019-03-05 | Drug Plastics & Glass Company, Inc. | Container assembly and closure with predetermined humidity and related method |
| US10737856B2 (en) | 2016-10-12 | 2020-08-11 | Drug Plastics & Glass Company, Inc. | Container and closure assembly with predetermined humidity and related method |
| US10913585B2 (en) | 2016-10-12 | 2021-02-09 | Drug Plastics & Glass Company, Inc. | Container and closure assembly with predetermined humidity and related method |
| US11612936B2 (en) * | 2020-02-24 | 2023-03-28 | University Of Science And Technology Beijing | Method for preparing oxygen-free passivated titanium or titanium-alloy powder product by means of gas-solid fluidization |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5633980B2 (en) | 1981-08-07 |
| JPS5314185A (en) | 1978-02-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4127503A (en) | Oxygen absorbent | |
| US4192773A (en) | Oxygen absorbent | |
| US4166807A (en) | Oxygen absorbent | |
| US4384972A (en) | Foodstuff freshness keeping agents | |
| US4337276A (en) | Method for storing produce and container and freshness keeping agent therefore | |
| US3419400A (en) | Packaging foods-production of oxygen-free packages | |
| US4366179A (en) | Oxygen and carbon dioxide absorbent and process for storing coffee by using the same | |
| US4552767A (en) | Method of packaging coffee with carbon dioxide sorbent | |
| US20090095941A1 (en) | Moisture-resistant deoxidant | |
| US4199472A (en) | Oxygen absorbent composition | |
| US3169068A (en) | Preservative of oxygen-labile substances, e.g., foods | |
| EP0547761B1 (en) | Oxygen absorber and method for producing same | |
| JP2901389B2 (en) | Oxygen scavenger | |
| US3946118A (en) | Process for retaining freshness of fruits, vegetables and cereals | |
| JPS6041986B2 (en) | oxygen absorber | |
| JPS5829069B2 (en) | Freshness preserving agent | |
| JP2658640B2 (en) | Oxygen scavenger | |
| JPS6147131B2 (en) | ||
| JPS626848B2 (en) | ||
| JPH0811056B2 (en) | Oxygen absorber | |
| JPS6233265B2 (en) | ||
| JPS6128374B2 (en) | ||
| JPS629376B2 (en) | ||
| JPS6120339B2 (en) | ||
| JPS6324738B2 (en) |